Metal Organic Frameworks for Gas Storage

ABSTRACT

Embodiments of the present disclosure describe methods of removing one or more compounds from a fluid comprising contacting a metal-organic framework (MOF) composition having a square-octahedral topology with a fluid containing one or more of CH 4  and O 2 , sorbing one or more of CH 4  and O 2  with the MOF composition, and storing one or more of the CH 4  and O 2  with the MOF composition.

BACKGROUND

Today there is an increasing global desire to reduce greenhouse gasemissions and develop clean alternative vehicle fuels. Methane (CH₄),the primary component of natural gas, is of particular interest as it isabundant and has lower CO₂ emission and more efficient combustion thanother hydrocarbons due its high H/C ratio. In addition toindustry-driven demand for stationary gaseous storage, globalgovernmental initiatives have created incentives to develop vehiculargaseous fuel storage.

Gas storage in porous materials has experienced significant developmentin recent years in various industrial applications related to energy,environment, and medicine. Among porous materials, metal organicframeworks (MOFs) are a versatile and promising class of crystallinesolid state materials which allow porosity and functionality to betailored towards various applications. MOF crystal chemistry uses amolecular building block (MBB) approach that offers potential toconstruct MOFs where desired structural and geometrical information areincorporated into the building blocks prior to the assembly process.Choosing an ideal blueprint net and isolating the reaction conditionsthat permit in situ consistent formation of the corresponding inorganicMBBs are the keys for successfully implementing this approach.

The challenges of constructing MOFs having tailored properties for gasstorage applications have limited the use of low cost materials such asaluminum and iron. In particular, low cost materials have not beendeveloped which satisfy the Department of Energy (DOE) CH4 gravimetricuptake target of 700 cm³ STP/g (0.5g/g) at recommended temperaturesbetween −40° C. and 85° C.

SUMMARY

In general, embodiments of the present disclosure relate to methods ofremoving one or more compounds from a fluid. It should be noted thatalthough the embodiments of this disclosure are described with respectto examples for gas storage, the embodiments described herein aregenerally applicable to many fields including gas molecule separation,catalysis, sensors, and proton conductivity.

Embodiments of the present disclosure describe a method of removing oneor more compounds from a fluid comprising contacting a metal-organicframework (MOF) composition having a square-octahedral topology with afluid containing one or more of CH₄ and O₂, wherein the MOF compositionincludes an organic ligand and a metal selected from aluminum, gallium,iron, scandium, titanium, chromium, and vanadium; sorbing one or more ofCH₄ and O₂ with the MOF composition; and storing one or more of the CH₄and O₂ with the MOF composition.

Embodiments of the present disclosure describe a method of removing oneor more compounds from a fluid comprising contacting a metal-organicframework (MOF) composition having a square-octahedral topology with afluid containing one or more of CH₄ and O₂, wherein the MOF compositionincludes a metal and an organic ligand selected from:amidetetracarboxylate, TCPT, TCDPN, TCDPA,2″,3″,5″,6″-tetrabromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″,5″-tribromo-5′,5 ″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,5″-dibromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,2″,3″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″-(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″,5″-bis(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,3,3′,3″,3″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid, 3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolic acid,3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid,3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolicacid,4,4′,4″,4″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayltetrakis(ethyne-2,1-diyl))tetrabenzoicacid,4,4′,4″,4″′-(((1,4-phenylenebis(ethyne-2,1-diyl))bis(benzene-5,1,3-triyl))tetrakis(ethyne-2,1-diyl))tetrabenzoicacid, 5″,5″″″′-(1,4-phenylenebis(ethyne-2,1-diyl))bis(([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″-dicarboxylicacid)),5″,5″″″′-(1,4-phenylenebis([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)), 0026BIS, 5,5′-(ethane-1,2-diyl)diisophthalic acid,(E)-5,5′-(diazene-1,2-diyl)diisophthalic acid,(E)-5,5′-(ethene-1,2-diyl)diisophthalic acid,5,5′-(ethyne-1,2-diyl)diisophthalic acid,(Z)-1,2-bis(3,5-dicarboxyphenyl)diazene 1-oxide, LigandC₄₂H₂₆O₈,4,4′,4″,4″′-(1,4-phenylenebis(azanetriyl))tetrabenzoic acid, andcombinations thereof; sorbing one or more of CH₄ and O₂; and storing oneor more of the sorbed CH₄ and sorbed O₂.

Embodiments of the present disclosure describe a method of removing oneor more compounds from a fluid comprising contacting a metal-organicframework (MOF) composition having a square-octahedral topology with afluid containing one or more of CH₄ and O₂, wherein the MOF compositionincludes an organic ligand and a metal selected from aluminum, gallium,iron, scandium, titanium, chromium, and vanadium; sorbing one or more ofCH₄ and O₂ with the MOF composition; storing one or more of the CH₄ andO₂ with the MOF composition; and desorbing one or more of the CH₄ and O₂from the MOF composition.

The details of one or more examples are set forth in the accompanyingdrawings and the description below. Other features, objects, andadvantages will be apparent from the description and drawings, and fromthe claims.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings illustrate non-limiting example embodiments ofthe invention.

FIG. 1A illustrates a block flow diagram of a method of storing one ormore compounds using a metal organic framework, according to one or moreembodiments of this disclosure.

FIG. 1B illustrates a ball-and-stick structure and a polyhedralrepresentation of a trimer molecular building block, according to one ormore embodiments.

FIG. 1C illustrates a ball-and-stick structure and a polyhedralrepresentation of a suitable organic ligand, according to one or moreembodiments.

FIG. 1D illustrates a ball-and-stick structure and a polyhedralrepresentation of a M-soc-MOF, according to one or more embodiments.

FIG. 1E illustrates a perspective view of a square-octahedral molecularorganic framework cage and network, according to one or more embodimentsof this disclosure.

FIG. 1F illustrates a X-ray diffraction data for a square-octahedralmolecular organic framework, according to one or more embodiments ofthis disclosure.

FIG. 2A illustrates gaseous adsorption isotherms for square-octahedralmolecular organic frameworks, according to one or more embodiments ofthis disclosure.

FIG. 2B illustrates thermal stability data for square-octahedralmolecular organic frameworks, according to one or more embodiments ofthis disclosure.

FIG. 3A illustrates absolute gravimetric adsorption uptakes of methanefor a square-octahedral molecular organic framework, according to one ormore embodiments of this disclosure.

FIG. 3B illustrates isosteric heat of adsorption for square-octahedralmolecular organic frameworks, according to one or more embodiments ofthis disclosure.

FIG. 4 illustrates adsorption gravimetric uptake of methane for variousMOF architectures, according to one or more embodiments of thisdisclosure.

FIG. 5 illustrates adsorption volumetric working uptake of methane forvarious MOF architectures, according to one or more embodiments of thisdisclosure.

FIG. 6A illustrates absolute carbon dioxide adsorption isotherms forvarious MOF architectures, according to one or more embodiments of thisdisclosure.

FIG. 6B illustrates excess and absolute hydrogen adsorption isothermsfor various MOF architectures, according to one or more embodiments ofthis disclosure.

FIG. 6C illustrates absolute oxygen adsorption isotherms for variousmolecular organic framework architectures, according to one or moreembodiments of this disclosure.

FIG. 6D illustrates absolute ethane, propane, n-butane and iso-butaneadsorption isotherms for various molecular organic frameworkarchitectures, according to one or more embodiments of this disclosure.

FIG. 7 illustrates experimental and simulated methane adsorption data,according to one or more embodiments of this disclosure.

FIGS. 8A-C illustrate simulated screenshots of methane adsorption atvarious pressures, according to one or more embodiments of thisdisclosure.

FIGS. 9A-B illustrate simulations of methane sorption at varioustemperatures, according to one or more embodiments of this disclosure.

FIG. 10 illustrates a ligand modification strategy schematic, accordingto one or more embodiments of this disclosure.

FIG. 11 illustrates simulated adsorption isotherms for variousisostructural metal organic frameworks, according to one or moreembodiments of this disclosure.

FIG. 12 illustrates simulated adsorption isotherms for variousisostructural metal organic frameworks, according to one or moreembodiments of this disclosure.

FIG. 13 illustrates a Rubotherm gravimetric-densimetric apparatusschematic, according to one or more embodiments of this disclosure.

DETAILED DESCRIPTION

The present invention is described with reference to the attachedfigures, wherein like reference numerals are used throughout the figuresto designate similar or equivalent elements. The figures are not drawnto scale and they are provided merely to illustrate the invention.Several aspects of the invention are described below with reference toexample applications for illustration. It should be understood thatnumerous specific details, relationships, and methods are set forth toprovide an understanding of the invention. One skilled in the relevantart, however, will readily recognize that the invention can be practicedwithout one or more of the specific details or with other methods. Inother instances, well-known structures or operations are not shown indetail to avoid obscuring the invention. The present invention is notlimited by the illustrated ordering of acts or events, as some acts mayoccur in different orders and/or concurrently with other acts or events.Furthermore, not all illustrated acts or events are required toimplement a methodology in accordance with the present invention.

Provided herein are M-soc-MOFs having improved surface area, porevolume, and volumetric and gravimetric working capacity. In particularare provided single crystal structures for the first three isoreticularseries of aluminum MOFs possessing soc topology and having highlypermanent microporosity and high thermal stability. In one embodiment, ahighly microporous MOF assembly comprises an aluminum trimer componentand a quadrangular ligand component. In some such embodiments, the MOFassembly has a Langmuir specific surface area of more than about 5000m²/g, more than about 5300 m²/g, more than about 6000 m²/g, or more thanabout 6300 m²/g. Embodiments provide aluminum MOFs possessing soctopology which require no heat to desorb stored gases such as CH₄, andare more easily activated by reducing the pressure to atmosphericpressure or using vacuum techniques not available to other highly porousmaterials known in the art. Methods provided herein allow for structuralalterations of aluminum-soc-MOFs which advantageously tune and/orenhance performance.

FIG. 1 illustrates a block flow diagram of a method 100 of removing oneor more compounds from one a fluid, according to an embodiment. Method100 includes contacting 102 one or more metal organic framework (MOF)compositions with a fluid, sorbing 104 one or more compounds from thefluid with the one or more MOF compositions, and storing 106 one or moresorbed compounds. In particular, method 100 includes contacting 102 oneor more M-soc-MOF compositions with a fluid and sorbing 104 one or morecompounds from the fluid with the one or more M-soc-MOF compositions.Contacting 102 can include mixing, bringing in close proximity,chemically contacting, physically contacting or combinations thereof.Fluids can include general liquids and gases. In some embodiments,fluids include industrial process fluids. Examples of specific fluidsinclude one or more of natural gas and biogas. Fluids can furthercomprise water, including water in a liquid form, a gaseous form, orcombinations thereof.

In one embodiment, sorbing 104 comprises absorbing. In one embodiment,sorbing 104 comprises adsorbing. In one embodiment, sorbing 104comprises a combination of adsorbing and absorbing. Sorbing 104 caninclude selective sorption (i.e., sorption of a single compound), orsimultaneous sorption (e.g., sorption of a plurality of compounds). TheM-soc-MOF compositions can sorb about 1% to about 99.9%, about 1% toabout 90%, about 1% to about 50% or about 1% to about 30% of one or morecompounds in a fluid. Sorbing 104 can occur at ambient temperature, atan elevated temperature, at a cooled temperature, or over a temperaturerange. In one embodiment, a temperature can be selectively changed tomanipulate sorption and/or desorption of different compounds. Sorbing104 can occur at ambient pressure, at an elevated pressure, at a cooledpressure, or over a pressure range. Sorbing 104 can occur attemperatures between about −80° C. and about 125° C., about −60° C. andabout 105° C. , or about −40° C. and about 85° C. In one embodiment,pressure can be selectively changed to manipulate sorption and/ordesorption of different compounds.

In addition to or in the alternative to, a concentration of one or moreM-soc-MOF compositions can be varied to affect a rate and/or magnitudeof sorbing 104. One or more of temperature, pressure and M-soc-MOFconcentration can be regulated to produce a simultaneous sorption ofcompounds, or a subsequent, step-wise sorption (i.e., in series) ofcompounds from a fluid. In series sorption generally includes sorbing aquantity of a first compound via a MOF, and subsequently sorbing aquantity of a second compound via the same MOF while at least a portionof the quantity of the first compound remains sorbed. Simultaneoussorption generally includes contacting a plurality of compounds with anMOF, and sorbing a quantity of each of the two compounds with the MOF.Storing 106 can occur at temperatures between about −80° C. and about125° C. , about −60° C. and about 105° C. , or about −40° C. and about85° C.

Storing 106 comprises maintaining a sorbed compound in a sorbed statefor a period of time. A sorbed state can include an adsorbed state, anabsorbed state, or combinations thereof. Maintaining a sorbed compoundin a sorbed state allows for the sorbed compound to change or oscillatebetween multiple sorbed states.

One compound which can be sorbed by an M-soc-MOF from a fluid is O₂. Onecompound which can be sorbed by an M-soc-MOF from a fluid is CH₄. O₂ andCH₄ can be simultaneously sorbed from a fluid by an M-soc-MOF. O₂ andCH₄ can be sorbed from a fluid in series by an M-soc-MOF. After sorbing104, one or more of O₂ and CH₄ can be stored 106 by the M-soc-MOF. In aspecific embodiment, O₂ can be stored 106 by an M-soc-MOF. In anotherspecific embodiment, CH₄ can be stored 106 by an M-soc-MOF. In anotherspecific embodiment, O₂ and CH₄ can be simultaneously stored 106 by anM-soc-MOF. Storing 106 can occur on board a vehicle, such as a seacraft,landcraft, aircraft, or spacecraft. Generally, the above sorption andstorage abilities are capable in the presence of water and H₂S, suchstability constituting an advantageous aspect unavailable from otherMOFs and industrial materials such as zeolites and activated carbon.Further, particular M-soc-MOFs, such as Al-soc-MOFs and Fe-soc-MOFs,exhibit further advantages from the use of lightweight and/orinexpensive materials.

M-soc-MOFs suitable for method 100 include M-soc-MOFs 200 comprising oneor more trimer molecular building blocks (TMBB) 201, as shown in FIG.1B, and one or more organic ligands 202, an example of which is shown inFIG. 1C. FIG. 1B illustrates a ball-and-stick structure 201′ and apolyhedral representation 201″ of a TMBB 201. FIG. 1C illustrates aball-and-stick structure 202′ and a polyhedral representation 202″ ofone example of a suitable organic ligand 202. Isostructuralsquare-octahedral M-soc-MOFs are built by linking the 6-connected TMBBsand the 4-connected organic ligands, resembling trigonal prismaticbuilding units (BUs) and rectangular BUs respectively, to generate anoverall 3D cationic framework having an edge-transitive (4,6)soc-topology.

A TMBB 201 comprises three metal carboxylate octahedra, each octahedralgenerally described as [MO₅(H₂O)], wherein M=a metal. A TMBB 201 can begenerally described as M₃O_(x)(CO₂)_(y). In some embodiments, a TMBB 201can be generally described as (M₃O(O₂CR)₆), wherein R is an organicmoiety, or any functional group capable of coordinating to the metal.The three metal octahedra are metal-centered, and all share one centralμ3-oxo anion. In each octahedron, the apical position can be occupied bya terminal water molecule. The metalcarboxylate clusters generate arigid node with fixed geometry involving multiple metaloxygencoordination bonds which induce the stability of the node andsubsequently enhance the thermal stability and overall rigidity of theframework. One example of a TMBB 201 can be described as[Ga₃O(CO₂)₆(H₂O)₃], or [Ga₃O(CO₂)₆] with the H₂O guest molecule speciesomitted for clarity. One example of a TMBB 201 can be described as[In₃O(CO₂)₆]. One example of a TMBB 201 can be described as[Al₃O(CO₂)₆]. One example of a TMBB 201 can be described as[Al₃O(CO₂)₆]. One example of a TMBB 201 can be described as[Fe₃O(CO₂)₆]. One example of a TMBB 201 can be described as[Sc₃O(CO₂)₆]. One example of a TMBB 201 can be described as[Cr₃O(CO₂)₆]. One example of a TMBB 201 can be described as [V₃O(CO₂)₆].

Suitable metals (M) include trivalent metals (i.e., metals capable ofexhibiting a +3 oxidation state). Trivalent metals include aluminum,scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel,copper, gallium, germanium, arsenic, yittrium, zirconium, niobium,molybdenum, palladium, silver, indium, tin, antimony, lanthanum, cerium,praseodymium, samarium, europium gadolinium, terbium, erbium, thulium,ytterbium, lutetium, tantalum, tungsten, rhenium, osmium, iridium,platinum, gold, lead, and bismuth. Particularly suitable trivalentmetals include gallium, indium, iron, scandium, and aluminum. The threetrivalent metals yield an overall cationic framework (+1 per formulaunit) that can be balanced, for example, by [Cl]⁻¹ ions. In such anexample, the disordered [Cl]⁻¹ ions occupy statistically two positionson the threefold axis with equal probability. A broad range of suitabletrivalent metals advantageously allows for M-soc-MOFs to be customizedfor particular purposes. For example, lighter trivalent metals canprovide an M-soc-MOF with increased sorption uptake per unit volume.

Each TMBB unit is linked by six separate organic ligands 202, as shownin FIG. 1B, to produce a novel 3D structure 200 having an soc-topology,as shown in FIG. 1D. Suitable ligands are tetradentate. Suitabletetradentate ligands include rectangular planar ligands. A generallysuitable ligand is a tetracarboxylate ligand.

One particular suitable ligand is3,3″,5,5″-tetrakis(4-carboxyphenyl)-p-terphenyl (TCPT):

One particular suitable ligand is3′,3″,5′,5″-tetrakis(4-carboxyphenyl)-1,4-diphenylnaphthalene (TCDPN):

One particular suitable ligand is3′,3″,5′,5″-tetrakis(4-carboxyphenyl)-9,10-diphenylanthracene (TCDPA):

One particular suitable ligand is2″,3″,5″,6″-tetrabromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid:

One particular suitable ligand is2″,3″,5″-tribromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″-dicarboxylicacid:

One particular suitable ligand is2″,5″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid:

One particular suitable ligand is2″,3″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid:

One particular suitable ligand is5′,5″′-bis(4-carboxyphenyl)-2″-(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid:

One particular suitable ligand is5′,5″-bis(4-carboxyphenyl)-2″,5″-bis(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid:

One particular suitable ligand is3,3′,3″,3″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid:

One particular suitable ligand is3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolicacid:

One particular suitable ligand is3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid:

One particular suitable ligand is3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolicacid:

One particular suitable ligand is4,4′,4″,4″-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayltetrakis(ethyne-2,1-diyl))tetrabenzoicacid:

One particular suitable ligand is4,4′,4″,4″′-(((1,4-phenylenebis(ethyne-2,1-diyl))bis(benzene-5,1,3-triyl))tetrakis(ethyne-2,1-diyl))tetrabenzoicacid:

One particular suitable ligand is5″,5″″″′-(1,4-phenylenebis(ethyne-2,1-diyl))bis(([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″-dicarboxylicacid)):

One particular suitable ligand is5″,5″″″′-(1,4-phenylenebis(([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)):

One particular suitable ligand is 0026BIS:

One particular suitable ligand is 5,5′-(ethane-1,2-diyl)diisophthalicacid:

One particular suitable ligand is(E)-5,5′-(diazene-1,2-diyl)diisophthalic acid:

One particular suitable ligand is amidetetracarboxylate, or5-(3,5-dicarboxybenzamido)isophthalic acid:

One particular suitable ligand is(E)-5,5′-(ethene-1,2-diyl)diisophthalic acid:

One particular suitable ligand is 5,5′-(ethyne-1,2-diyl)diisophthalicacid:

One particular suitable ligand is(Z)-1,2-bis(3,5-dicarboxyphenyl)diazene 1-oxide:

One particular suitable ligand is4,4′,4″,4″′-(1,4-phenylenebis(azanetriyl))tetrabenzoic acid:

One particular suitable ligand is 3,3′,5,5′-azobenzenetetracarboxylate,or 5,5′-(hydrazine-1,2-diyl)diisophthalic acid:

One particular suitable ligand is3,3′″,5,5′″-tetrakis{4″″-(4″″′-carboxy-[1″″,1″″′-biphenyl])}-1,1′:4′,1″:4″,1″′-quaterphenyl:

FIG. 1D illustrates a ball-and-stick structure 200′ and a polyhedralrepresentation 200″ of a suitable M-soc-MOF 200 comprised of a pluralityof 6-connected TMBBs 201 networked by organic tetradentate planarligands 202. In FIG. 1D, hydrogen atoms, water molecules, and [NO₃]—ions are omitted for clarity. One example M-soc-MOF 200 can be describedas [In₃O(C₁₆N₂O₈H₆)_(1.5)(H₂O)₃](H₂O)₃(NO₃). All such M-soc-MOFs arecharacterized by an soc-topology, and can generally be denoted asM-soc-MOFs. The soc-topology of M-soc-MOF 200 provides unique structurefeatures, including the presence of isolated nanometer-scalecarcerand-like capsules, which anchor nitrate ions, and which arestrictly accessible through the two main channels by very restrictedwindows. Such characteristics provide high, localized charge densityadvantageous for chemical and physical sorption of compounds.

Other interesting structural features of the crystalline structure areits two types of infinite channels. The first type is hydrophilic, dueto the water molecules coordinated to the indium centers which arepointed inside these channels. Guest water molecules occupy theremaining free volume in these channels and form hydrogen bonds withcoordinated water molecules. The second type of channels can be guestfree, and have an approximately 1 nm diameter.

M-soc-MOFs can have a BET surface area of at least about 800 m²/g, atleast about 900 m²/g, at least about 1,000 m²/g, at least about 1,200m²/g, at least about 1,400 m²/g, or at least about 1,600 m²/g. In aspecific embodiment, an M-soc-MOF has a BET surface area of at leastabout 800 m²/g. In a specific embodiment, an M-soc-MOF has a BET surfacearea of about 1,000 m²/g. In a specific embodiment, an M-soc-MOF has aBET surface area of about 1,000 m²/g to about 1,600 m²/g.

M-soc-MOFs can have an average pore volume of at least about 0.2 cm³/g,at least about 0.25 cm³/g, at least about 0.3 cm³/g, at least about 0.45cm³/g, at least about 0.6 cm³/g, or at least about 0.65 cm³/g. In aspecific embodiment, an M-soc-MOF has an average pore volume of at leastabout 0.2 cm³/g. In a specific embodiment, an M-soc-MOF has an averagepore volume of about 0.3 cm³/g. In a specific embodiment, an M-soc-MOFhas an average pore volume of about 0.3 cm³/g to about 0.65 cm³/g.

In one embodiment, a representative MOF unit cell comprises a pluralityof aluminum components networked with a plurality of ligand components.For example, the MOF unit cell can comprise soc topology, having 86-connected aluminum components and 6 4-connected ligands. In someembodiments the aluminum components are aluminum trimers. In someparticular embodiments the aluminum trimer is a μ3-oxo-centered trimerof octahedral AlO₆. In some embodiments the ligand component is aquadrangular ligand. In some particular embodiments the ligand componentis a 3,3″,5,5″-tetrakis(4-carboxyphenyl)-p-terphenyl (TCPT) tetratopicligand, which can act as a rectangular MBB. Accordingly, arepresentative MOF unit cell can comprise 8 AlO₆ trimers networked with6 TCPT ligands. This Al-soc-MOF-2 unit cell is characterized by a cubicshaped cage defined by the AlO₆ trimers at the corners and the ligandsoccupying the faces of the cage, resulting in a soc-a network topologyas shown in FIG. 1D. This Al-soc-MOF-2 unit cell can have one or more ofa diameter of about 14.3 Å, apertures measuring about 9 Å (consideringvdW radii), and two well-defined 1D infinite channels about 14 Å. Whensuch unit cells are agglomerated, the 1D infinite channels canapproximately reach the border of the micro-porous materials, as shownin FIG. 1E. The Langmuir surface area for the Al-soc-MOF-2 architecturewas estimated to be ca. 7118 m²/g, with a pore volume of 2.3 cm³/g.Al-soc-MOF-2 unit cells can be synthesized by reacting TCPT andAlCl₃.6H₂O in an N,NDMF/CH₃CN/HNO₃ solution. Such a reaction yields purephase cube-shaped crystals as shown in the powder X-ray diffractionpattern of FIG. 1F, which can be represented by[Al₃(C₆₆O₈H₂₆)_(1.5)(H₂O)₃].(Cl).

Altering the ligands of the Al-soc-MOF-2 embodiment can provide variousisoreticulars having similar topologies and thus similarly usefulphysical properties. In one embodiment, the phenyl ring located in thecore of the TCPT ligand can be substituted by (1,4-substituted)naphthalene to provide the naphthalene functionalized ligand3′,3″,5′,5″-tetrakis(4-carboxyphenyl)-1,4-diphenylnaphthalene (TCDPN).The TCDPN ligand can be networked with aluminum trimers as in theAl-soc-MOF-2 embodiment to provide a Naphth-Al-soc-MOF-2 isoreticular.In another embodiment, the phenyl ring located in the core of the TCPTligand can be substituted by (9,10-substituted) anthracene to providethe anthracene functionalized ligand3′,3″,5′,5″-tetrakis(4-carboxyphenyl)-9,10-diphenylanthracene (TCDPA).The TCDPA ligand can be networked with aluminum trimers as in theAl-soc-MOF-2 embodiment to provide an Anth-Al-soc-MOF-2 isoreticular.

The Langmuir surface area for the Naphth-Al-soc-MOF-2 andAnth-Al-soc-MOF-2 architectures were estimated to be ca. 6300 m²/g and5350 m²/g, respectively. Naphth-Al-soc-MOF-2 and Anth-Al-soc-MOF-2architectures have pore volumes of 2.1 cm³/g and 1.8 cm³/g,respectively.

Naphth-Al-soc-MOF-2 and Anth-Al-soc-MOF-2 unit cells can each besynthesized by reacting TCDPN and TCDPN, respectively, with AlCl₃.6H₂Oin an N,NDMF/CH₃CN/HNO₃ solution. Such a reaction yields homogeneouscube-shaped crystals which can each be represented by[Al₃(Ligand)_(1.5)(H₂O)₃].(Cl).

Al-soc-MOF architectures provided herein, including Al-soc-MOF-2,Naphth-Al-soc-MOF-2, and Anth-Al-soc-MOF-2 architectures, exhibit type-Iadsorption isotherms which are fully reversible. This quality isrepresentative of porous materials with permanent microporosity. Forexample, as shown in FIG. 2A, adsorption isotherms for nitrogen (at 77K) and argon (at 87K) are given for Al-soc-MOF-2. Indeed, the Al-soc-MOFarchitectures provided herein exhibit high resistance to pore collapseand high thermal stability. This permanent microporosity is demonstratedby harmonized experimental and optimal theoretical values for porevolume on each Al-soc-MOF architecture, which indicates no or minimalpore collapse during sample activation under vacuum. Such a feature isadvantageous in that highly porous MOF architectures typically collapseunder vacuum. Further, the Al-soc-MOF architectures provided hereinpreserve their optimal porosity on heating up to 360° C. under vacuum, afeature rarely observed for highly porous MOFs. As shown in FIG. 2B, thehigh thermal stability was verified using variable temperature powderX-ray diffraction studies (VT-PXRD. It can be seen that Al-soc-MOF-2architectures retain crystallinity up until at least 400° C.

Methane storage capabilities for the Al-soc-MOF architectures providedherein is illustrated in FIG. 3A, wherein the absolute gravimetricadsorption uptakes of CH₄ for various Al-soc-MOF-2 isotherms are givenover a range of pressures up to 85 bar. As shown, the Al-soc-MOF-2architecture exhibits the highest ever CH₄ gravimetric uptakes (ca. 361cm³/g) for MOFs at the standard conditions (298 K and 35 bar). The DOECH₄ gravimetric uptake target of 700 cm³ STP/g (0.5 g/g) was largelyachieved for the Al-soc-MOF-2 isotherms below 288 K in the range ofpressure between 50 (258 K) and 85 (288 K) bar. FIG. 3B shows isostericheat of adsorption for Al-soc-MOF-2.

FIG. 4 shows that the Al-soc-MOF-2 architecture exhibits highergravimetric uptakes at 35, 50 and 70 bar in comparison to competitiveMOF materials in the same pressure conditions at 298 K. Further, FIG. 5provides a deep analysis of the CH₄ storage capabilities at thevolumetric scale which shows that Al-soc-MOF-2 exhibits increasedworking volumetric uptakes (from 201 to 264 cm3STP/cm3) with decreasingtemperature (from 298 to 258 K) in the pressure range between 5 bar(desorption) and 70-80 bar (adsorption). This in contrast to all knowncompetitive MOF materials for CH₄ storage which exhibit a decreasingworking CH₄ storage capacity trend with decreasing temperature forUTSA-76, HKUST-1, Ni-MOF-74 and PCN-14.

Without being held to a particular mechanism or theory, an explanationfor the inverted working storage capacity trend for Al-soc-MOF-2 is thelow unused CH₄ uptake below 5 bar and the linear trend of the CH₄isotherms at high pressure, which is a desirable feature for gas storagemedia. In contrast to all known competitive MOFs, Al-soc-MOF-2 exhibitsrelatively low CH₄ heat of adsorption across the CH₄ loading range. Asshown in FIG. 3B, the CH₄ heat of adsorption is only slightly higherthan the CH₄ latent heat of evaporation across the loading range. Theincreasing interaction trend at high CH₄ loading can, in part, beexplained by the multilayer adsorption induced by the promoted CH₄—CH₄interaction at high pressure. The combined effects at low and highpressure are contributing factors for the increased CH₄ working uptakesduring temperature reduction. It is important to mention that at 298 Kand 5-80 pressure working range, Al-soc-MOF-2 exhibits the secondhighest working capacity (201 cm³STP/cm³) vs. 230 cm³STP/cm³ reportedrecently for MOF-519.

Storage capacity of Al-soc-MOF-2 was tested for other importantcommodities including O₂, CO₂ and other condensable light hydrocarbons(ethane (C₂H₆) propane (C₃H₈), n-butane (n-C₄H₁₀) and iso-butane(iso-C₄H₁₀)). FIGS. 6A-D illustrate Al-soc-MOF-2 gas adsorptionperformance. As shown in FIG. 6A, Al-soc-MOF-2 exhibited also a record 2g/g (1020 cm³STP/g) of absolute gravimetric CO₂ uptake at 40 bar amongmicroporous MOFs in comparison to the 1.5 g/g absolute gravimetric CO₂uptake of MOF-177. Al-soc-MOF-2 exhibited a working capacity between 5and 40 bar of 1.75 g/g (891 cm³STP/g) as compared to the workingcapacity of 1.28 g/g (652 cm³STP/g) for MOF-177. As shown in FIG. 6C,Al-soc-MOF-2 exhibits a record 29 mmol/g of absolute gravimetric O₂uptake at 140 bar, which is considerably higher than competitiveproducts HKUST-1 (13.2 mmol/g) and NU-125 (17.4 mmol/g). An impressiveworking capacity between 5 and 140 bar of 27.5 mmol/g is furtherdemonstrated in FIG. 6C for the Al-soc-MOF-2 architecture, especially incomparison to the 11.8 and 15.4 mmol/g working capacities of HKUST-1 andNU-125, respectively.

Additionally, light hydrocarbons such as C₂H₆, C₃H₈, n-C₄H₁₀ andiso-C₄H₁₀ (referenced as R600a refrigerant) are excellent refrigerantsand their combination with excellent highly porous adsorbents couldenhance the cooling power in cooling in adsorption based chillers. Asseen in FIG. 6D, Al-soc-MOF-2 exhibited the highest uptake for C₂H₆,C₃H₈, n-C₄H₁₀ and iso-C₄H₁₀ reported for microporous MOFs. In additionthe complete desorption process of this refrigerant from theAl-soc-MOF-2 is possible at very mild conditions (298-323 K). FinallyAl-soc-MOF-2 exhibit excellent H₂ storage at 77 K (ca. 11 wt %) incomparison to other existing highly porous materials.

As shown in FIG. 7, an excellent agreement is observed between a CH₄sorption GCMC simulation and experimental isotherms at 298 K. In FIG. 7,circles represent simulation data and squares represent experimentaldata. FIGS. 8A-C show simulation snapshots illustrating the adsorptionof CH₄ in the Al-soc-MOF-2 pores at 5 bar, 35 bar, and 65 bar,respectively. In FIGS. 8A to 8B to 8C, an increased saturation of theAl-soc-MOF matrix by CH₄ molecules (light spheres) is observed. FIGS.9A-B illustrate additional simulations of CH₄ sorption in Al-soc-MOF-2at 298K, 295 K, 273 K, and 258 K, with results provided from bothgravimetric and volumetric bases. The simulation data confirm theexperimental results shown in FIG. 3A.

The Al-soc-MOF series embodiments presented above (i.e., Al-soc-MOF-2,Naphth-Al-soc-MOF-2, and Anth-Al-soc-MOF-2) are promising materials withpotential use in gas storage and separation applications. When used asblueprint nets, these materials permit the construction of MOFs withinteresting structural features having defined, porous, and highlyaccessible channels/cavities. The Al-soc-MOF-2 series showed extremelyhigh gas storage density for H₂, CH₄, and CO₂. Any non-optimal porosityas exemplified from the intermediate surface area and pore volumeexhibited by the Al-soc-MOF-2 series can be remedied in otherembodiments through soc-MOF alteration strategies. Specifically, ligandcomponents of soc-MOF embodiments can be altered to increase performanceand physical attributes, such as accessible porosity. It is important tonote that while increasing the surface area and pore volume of a porousmaterial is important to enhancing CH₄ gravimetric uptakes, thevolumetric working capacity is a crucial parameter to assess thematerial's performance towards CH₄ storage. It represents the usableamount of CH₄ deduced from subtracting the uptake at the deliverypressure (5 bar) from the uptake at the maximum adsorption pressure (35bar or higher).

The verified simulation methods discussed above were further utilized toalter ligand construction for overall Al-soc-MOF architectureperformance optimization for storage of valuable commodities such asCH₄, H₂, CO₂ and O₂. Ligand alteration can include elongation andcontraction of ligands through removal or addition of constituentgroups. Ligand alteration can additionally or alternatively includereplacing one or more ligand constituents. In one embodiment, ligandalteration includes replacing one or more representative X constituentswith 2 or more constituent groups. As shown in FIG. 10, a representativeligand for Al-soc-MOF provided herein comprises 7 core constituentgroups, labeled either X or Y. In one embodiment, the Y constituentgroup of the representative ligand can comprise an aryl or heteroarylconstituent. In one embodiment, the X constituent group of therepresentative ligand can comprise an aryl, functionalized aryl (R-aryl,R=n-CH₂, CF₃, Br, Cl, etc.), polyaryl, heteroaryl, or alkyneconstituent. Ligand alteration is applicable to aluminum, iron, gallium,indium, vanadium, chromium, titanium, and scandium soc-MOF analogues.

CH₄ adsorption for Al-soc-MOF embodiments with ligands altered using thestrategy illustrated in FIG. 10 was calculated using GCMC simulations.FIG. 11 and FIG. 12 illustrate simulated CH₄ adsorption isotherms andworking capacities for various isostructural Al-soc-MOFs. In FIG. 11,the working capacities of3,3′,3″,3″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetra)tetra propionic acid(denoted Ligand A in FIG. 11),3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolic acid(denoted Ligand B in FIG. 11),3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolicacid (denoted Ligand C in FIG. 11),3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid (denoted Ligand D in FIG. 11), TCPT, and LigandC₄₂H₂₆O₈ weremeasured across a range of pressures to determine a relation betweenworking capacity and the distance between the X moieties (shown in FIG.10). The same strategy was followed with additional tetracarboxylateligands as shown in FIG. 11. The results shown in FIGS. 10-11 show thatworking volumetric capacity can be enhanced by shortening the distancebetween the X moieties. Such an alteration creates isostructuralAl-soc-MOFs with slightly lower porosity but shifted isothermscurvatures which indicate higher capacity at lower pressures. Incontrast, increasing the distance in X-branches or X-core moieties ledto other isostructural Al-soc-MOFs with enhanced gravimetric uptake butwith much lower volumetric capacity.

Adsorption equilibrium measurements of pure gases (i.e., CO₂, CH₄, H₂,C₂H₆, C₃H₈ and n-C₄H₁₀) was performed using a Rubothermgravimetric-densimetric apparatus (Bochum, Germany) as shown in FIG. 13,comprising a magnetic suspension balance (MSB) and a network of valves,mass flowmeters and temperature and pressure sensors. The MSB overcomesthe disadvantages of other commercially available gravimetricinstruments by separating the sensitive microbalance from the sample andthe measuring atmosphere and is able to perform adsorption measurementsacross a wide pressure range, i.e. from 0 to 20 MPa. The adsorptiontemperature may also be controlled within the range of 77 K to 423 K. Ina typical adsorption experiment, the adsorbent is precisely weighed andplaced in a basket suspended by a permanent magnet through anelectromagnet. The cell in which the basket is housed is then closed andvacuum or high pressure is applied. The gravimetric method allows thedirect measurement of the reduced gas adsorbed amount. Correction forthe buoyancy effect is required to determine the excess and absoluteadsorbed amount using equations 1 and 2, where V_(adsorbent) and V_(ss)and V_(adorbed) phase refer to the volume of the adsorbent, the volumeof the suspension system and the volume of the adsorbed phase,respectively.

Ω=m _(absolute)−ρ_(gas)(V _(adsorbent) +V _(ss) +V _(adsorbed-phase))  (1)

Ω=m _(excess)ρ_(gas)(V _(adsorbent) +V _(ss))   (2)

The buoyancy effect resulted from the adsorbed phase maybe taken intoaccount via correlation with the pore volume or with the theoreticaldensity of the sample. These volumes are determined using the heliumisotherm method by assuming that helium penetrates in all open pores ofthe materials without being adsorbed. The density of the gas isdetermined using Refprop equation of state (EOS) database and checkedexperimentally using a volume-calibrated titanium cylinder. By weighingthis calibrated volume in the gas atmosphere, the local density of thegas is also determined. Simultaneous measurement of adsorption capacityand gas phase density as a function of pressure and temperature istherefore possible.

The pressure is measured using two Drucks high pressure transmittersranging from 0.5 to 34 bar and 1 to 200 bar, respectively, and one lowpressure transmitter ranging from 0 to 1 bar. Prior to each adsorptionexperiment, about 200 mg of sample is outgassed at 473 K at a residualpressure 10-6 mbar. The temperature during adsorption measurements isheld constant by using a thermostated circulating fluid.

What is claimed is:
 1. A method of removing one or more compounds from afluid, comprising: contacting a metal-organic framework (MOF)composition having a square-octahedral topology with a fluid containingone or more of CH₄ and O₂, wherein the MOF composition includes anorganic ligand and a metal selected from aluminum, gallium, iron,scandium, titanium, chromium, and vanadium; sorbing one or more of CH₄and O₂ with the MOF composition; and storing one or more of the CH₄ andO₂ with the MOF composition.
 2. The method of claim 1, wherein theorganic ligand is selected from tetradentate organic ligands.
 3. Themethod of claim 1, wherein the organic ligand is selected fromtetracarboxylate ligands.
 4. The method of claim 1, wherein the organicligand is selected from rectangular planar organic ligands.
 5. Themethod of claim 1, wherein the organic ligand is selected from:amidetetracarboxylate, 3,3′,5,5′-azobenzenetetracarboxylate, TCPT,TCDPN, TCDPA,2″,3″,5″,6″-tetrabromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″,5″-tribromo-5′,5″-bis (4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylic acid,2″,5″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″-dibromo-5′,5″′-bis (4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylic acid,5′,5″-bis(4-carboxyphenyl)-2″-(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″,5″-bis(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,3,3′,3″,3′″-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid,3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolicacid,3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid,3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolicacid,4,4′,4″,4″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayltetrakis(ethyne-2,1-diyl))tetrabenzoicacid,4,4′,4″,4″′-(((1,4-phenylenebis(ethyne-2,1-diyl))bis(benzene-5,1,3-triyl))tetrakis(ethyne-2,1-diyl))tetrabenzoicacid,5″,5″″″′-(1,4-phenylenebis(ethyne-2,1-diyl))bis(([1,1′:4′,1″:3″,1″:4′″,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)), 5″,5″″″′-(1,4-phenylenebis([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″″-dicarboxylic acid)), 0026BIS,5,5′-(ethane-1,2-diyl)diisophthalic acid,(E)-5,5′-(diazene-1,2-diyl)diisophthalic acid,(E)-5,5′-(ethene-1,2-diyl)diisophthalic acid,5,5′-(ethyne-1,2-diyl)diisophthalic acid, (Z)-1,2-bis (3,5-dicarboxyphenyl)diazene 1-oxide, LigandC₄₂H₂₆O₈,4,4′,4″,4″′-(1,4-phenylenebis(azanetriyl))tetrabenzoic acid, andcombinations thereof.
 6. The method of claim 1, wherein the MOFcomposition stores one or more of CH₄ and O₂ at temperatures rangingfrom about −80° C. to about 125° C.
 7. The method of claim 1, whereinthe MOF composition stores one or more of CH₄ and O₂ at pressures up toabout 85 bar or less.
 8. The method of claim 1, further comprisingdesorbing one or more of the CH₄ and O₂.
 9. The method of claim 8,wherein heat is not required to desorb one or more of the CH₄ and O₂.10. The method of claim 1, wherein the fluid comprises one or more ofnatural gas and biogas.
 11. A method of removing one or more compoundsfrom a fluid, comprising: contacting a metal-organic framework (MOF)composition having a square-octahedral topology with a fluid containingone or more of CH₄ and O₂, wherein the MOF composition includes a metaland an organic ligand selected from: amidetetracarboxylate, TCPT, TCDPN,TCDPA,2″,3″,5″,6″-tetrabromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3′″,1″″-quinquephenyl]-4,4″-dicarboxylicacid,2″,3″,5″-tribromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,5″-dibromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 5′,5″′-bis(4-carboxyphenyl)-2″-(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″,5″-bis(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,3,3′,3″,3″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid,3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolicacid,3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid, 3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolic acid,4,4′,4″,4″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayltetrakis(ethyne-2,1-diyl))tetrabenzoic acid,4,4′,4″,4″′-(((1,4-phenylenebis(ethyne-2,1-diyl))bis(benzene-5,1,3-triyl))tetrakis(ethyne-2,1-diyl))tetrabenzoicacid,5″,5″″″′-(1,4-phenylenebis(ethyne-2,1-diyl))bis(([1,1′:4′,1″:3″,1″:4′″,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)),5″,5″″″′-(1,4-phenylenebis([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)), 0026BIS , 5,5′-(ethane-1,2-diyl)diisophthalic acid,(E)-5,5′-(diazene-1,2-diyl)diisophthalic acid,(E)-5,5′-(ethene-1,2-diyl)diisophthalic acid,5,5′-(ethyne-1,2-diyl)diisophthalic acid, (Z)-1,2-bis(3,5-dicarboxyphenyl)diazene 1-oxide, LigandC₄₂H₂₆O₈,4,4′,4″,4″′-(1,4-phenylenebis(azanetriyl))tetrabenzoic acid, andcombinations thereof; sorbing one or more of CH₄ and O₂; and storing oneor more of the sorbed CH₄ and sorbed O₂.
 12. The method of claim 11,wherein the metal is selected from aluminum, gallium, indium, iron,scandium, titanium, chromium, or vanadium.
 13. The method of claim 11,wherein the MOF composition stores one or more of CH₄ and O₂ attemperatures ranging from about −80° C. to about 125° C.
 14. The methodof claim 11, wherein the MOF composition stores one or more of CH₄ andO₂ at pressures up to about 85 bar or less.
 15. The method of claim 11,further comprising desorbing one or more of the CH₄ and O₂.
 16. Themethod of claim 15, wherein heat is not required to desorb one or moreof the CH₄ and O₂.
 17. The method of claim 11, wherein the fluidcomprises one or more of natural gas and biogas.
 18. A method ofremoving one or more compounds from a fluid, comprising: contacting ametal-organic framework (MOF) composition having a square-octahedraltopology with a fluid containing one or more of CH₄ and O₂, wherein theMOF composition includes an organic ligand and a metal selected fromaluminum, gallium, iron, scandium, titanium, chromium, and vanadium;sorbing one or more of CH₄ and O₂ with the MOF composition; storing oneor more of the CH₄ and O₂ with the MOF composition; and desorbing one ormore of the CH₄ and O₂ from the MOF composition.
 19. The method of claim18, wherein the organic ligand is selected from: amidetetracarboxylate,3,3′,5,5′-azobenzenetetracarboxylate, TCPT, TCDPN, TCDPA,2″,3″,5″,6″-tetrabromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″,5″-tribromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,5″-dibromo-5′,5″-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid, 2″,3″-dibromo-5′,5″′-bis(4-carboxyphenyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″-(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,5′,5″-bis(4-carboxyphenyl)-2″,5″-bis(trifluoromethyl)-[1,1′:3′,1″:4″,1″′:3″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid,3,3′,3″,3″′-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid,3,3′,3″,3″′-(ethyne-1,2-diylbis(benzene-5,1,3-triyl))tetrapropiolicacid,3,3′,3″,3″′-(2′,3′,5′,6′-tetramethyl-[1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayl)tetrapropiolicacid, 3,3′,3″,3″′-(ethyne-1,2-diylbis(2,4,6-trimethylbenzene-5,1,3-triyl))tetrapropiolic acid,4,4′,4″,4″-([1,1′:4′,1″-terphenyl]-3,3″,5,5″-tetrayltetrakis(ethyne-2,1-diyl))tetrabenzoicacid,4,4′,4″,4″′-(((1,4-phenylenebis(ethyne-2,1-diyl))bis(benzene-5,1,3-triyl))tetrakis(ethyne-2,1-diyl))tetrabenzoic acid,5″,5″″″′-(1,4-phenylenebis(ethyne-2,1-diyl))bis(([1,1′:4′,1″:3″,1″:4′″,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)),5″,5″″″′-(1,4-phenylenebis([1,1′:4′,1″:3″,1″′:4″′,1″″-quinquephenyl]-4,4″″-dicarboxylicacid)), 0026BIS, 5,5′-(ethane-1,2-diyl)diisophthalic acid,(E)-5,5′-(diazene-1,2-diyl)diisophthalic acid,(E)-5,5′-(ethene-1,2-diyl)diisophthalic acid,5,5′-(ethyne-1,2-diyl)diisophthalic acid, (Z)-1,2-bis (3,5-dicarboxyphenyl)diazene 1-oxide, LigandC₄₂H₂₆O₈,4,4′,4″,4″′-(1,4-phenylenebis(azanetriyl))tetrabenzoic acid, andcombinations thereof.
 20. The method of claim 18, wherein the MOFcomposition stores one or more of CH₄ and O₂ at temperatures rangingfrom about −80° C. to about 125° C. and/or at pressures up to about 85bar or less.